Abd. Hamid, Mohd. Kamaruddin and Ibrahim, Norazana and Ibrahim, Kamarul Asri and Ahmad, Arshad (2006) Simulation of hydrogen production for mobile fuel cell applications via autothermal reforming of methane. In: 1st International Conference on Natural Resources Engineering & Technology 2006, 24-25th July 2006, Putrajaya, Malaysia.
PDF (Full text)
This paper presents a simulation of catalytic autothermal reforming (ATR) of methane (CH4) for hydrogen (H2) production. ATR is essentially an oxidative steam reforming, which combines the exothermic partial oxidation (PO) with the endothermic steam reforming (SR) under thermally neutral conditions. A model is developed using HYSYS 2004.1 to simulate the conversion behavior of the reformer. The model covers all aspects of major chemical kinetics and heat and mass transfer phenomena in the reformer. The ATR and preferential oxidation (PrOx) processes is modeled using conversion reactor, while the water gas shift (WGS) process is modeled using equilibrium reactor within HYSYS environment. The conditions used for high CH4 conversion and high H2 yield are at air to fuel ratio of 2.5 and water to fuel ratio of 1.5. Under this condition, CH4 conversion of 100% and H2 yield of 44% on wet basis can be achieved and the system efficiency is about 87.7%.
|Item Type:||Conference or Workshop Item (Paper)|
|Additional Information:||Organized by Faculty of Chemical and Natural Resources Engineering, UTM|
|Uncontrolled Keywords:||Methane; autothermal reforming; HYSYS simulation; fuel cell|
|Subjects:||T Technology > TP Chemical technology|
|Divisions:||Chemical and Natural Resources Engineering (Formerly known)|
|Deposited By:||Pn Khairulbahiyah Yaakub|
|Deposited On:||15 Feb 2007 05:32|
|Last Modified:||01 Jun 2010 02:42|
Repository Staff Only: item control page